Maleic Anhydride Physical and Chemical Properties: Complete Technical Data Sheet

Apr 15, 2026

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Maleic Anhydride · Melting Point · Boiling Point · CAS 108-31-6 · Physical Properties · Data Sheet

Maleic Anhydride Physical & Chemical Properties:
Complete Technical Data Sheet

Melting & boiling points · Density · Vapour pressure · Solubility · Reactivity · QC methods · Incoming inspection

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⚡ 1. Quick Reference Data Card

🔬 Maleic Anhydride - Key Properties at a Glance (CAS 108-31-6)

Molecular Weight
98.06
g/mol
Melting Point ⭐
52.8
°C
Boiling Point
202
°C @ 760 mmHg
Flash Point
102
°C (closed cup)
Density (solid)
1.48
g/cm³ @ 20°C
Purity (comm.)
≥99.0%
standard grade
DG Class
4.1
UN 2215, PG III

🌡️ 2. Thermal Properties: Melting, Boiling & Flash Points

Thermal Property Value Method / Conditions Industrial Significance
Melting point ⭐ 52.8 °C ASTM E794 / capillary method; sharp transition for pure MAH Defining handling property - MAH is SOLID below 52.8°C. All industrial processing requires heating to 60–80°C first. Suppressed mp (below 52°C) indicates maleic acid contamination.
Crystallisation point ⭐ ≥52.5 °C ASTM E794; specification QC parameter Primary purity QC test - maleic acid (mp 138°C) and fumaric acid act as freezing-point depressants; crystallisation point below 52°C is a reject criterion
Boiling point 202 °C (760 mmHg) Atmospheric; pure compound High bp ensures minimal MAH loss by evaporation during synthesis (60–200°C range); distillation for purification requires vacuum (80–100°C at 1–5 mmHg)
Flash point ⭐ 102 °C (CC) Pensky-Martens closed cup; flammable liquid when molten Molten MAH above 102°C is a flammable liquid - fire risk in heated vessels. UPR synthesis (150–220°C) must use inert atmosphere (N₂) and explosion-proof equipment ⚠️
Auto-ignition temperature 477 °C ASTM E659 Well above synthesis temperatures; not a spontaneous ignition risk under normal process conditions; relevant for hot-work permit assessments near MAH lines
Dust explosive limits MEC ~30–50 g/m³ Minimum explosive concentration (dust cloud) MAH dust is explosible - Zone 22 dust hazard area classification may apply in flake handling areas; enclosed bag-tipping stations with dust extraction required ⚠️
LEL / UEL (vapour) LEL 1.4% / UEL 7.1% v/v As vapour above liquid MAH Relevant for heated tank venting design; at normal melt temperatures (60–80°C) vapour concentration is low; key concern in distillation column design above 100°C
Thermal decomposition onset > 280 °C TGA in N₂; onset ~280°C; rapid above 350°C MAH is thermally stable well above UPR synthesis temperatures (160–220°C); decomposition gives fumaric acid, CO, CO₂ at elevated temperatures; avoid overheating beyond 250°C

⚠️ Critical safety note - dual fire hazard: Maleic anhydride presents two distinct fire hazards that must be managed separately: (1) Solid/dust fire hazard (ambient) - MAH flakes are a combustible solid and the dust is explosible (Class 4.1 DG); dust accumulation in bag-handling areas requires ATEX dust zone classification; (2) Flammable liquid hazard (molten, >102°C) - once melted for synthesis, MAH becomes a flammable liquid; synthesis reactors operating above flash point require inert atmosphere, explosion-proof equipment, and no ignition sources. Both hazard modes must be addressed in site ATEX/DSEAR and COSHH/HAZOP assessments.

❄️🌡️ 3. Solid vs Liquid MAH: Property Differences

Because maleic anhydride crosses from solid to liquid at 52.8 °C - a temperature routinely encountered in both storage and processing environments - engineers working with MAH must be familiar with how its key properties change across this phase transition.

Property Solid MAH (<52.8°C) Molten MAH (60–100°C) Process Implication
Density 1.48 g/cm³ 1.31 g/cm³ (at 60°C) ~11% volume expansion on melting; tank capacity calculations must account for melt density; 1,000 kg solid → ~763 L molten
Vapour pressure <0.01 mmHg (20°C) ~0.5 mmHg (60°C); ~5 mmHg (100°C) Inhalation risk negligible from solid; significant from molten MAH above 60°C - LEV mandatory for all open-vessel molten MAH operations
Fire hazard mode Combustible solid + dust explosion ⚠️ Flammable liquid (fp 102°C) ⚠️ Different ATEX zone classification for solid handling area vs liquid processing area; different emergency response procedures
Primary inhalation hazard Dust (particulate) Vapour / mist Solid handling: P3 FFP3 dust mask + full face shield; Molten handling: OV/P3 combination respirator + full face shield
Skin contact hazard Irritant → corrosive (moisture + sweat activates) Corrosive + thermal burn ⚠️ Molten MAH causes instant corrosive chemical burn AND thermal burn - PVC or rubber chemical splash suit mandatory for any molten MAH handling
Moisture reactivity Slow surface hydrolysis → caking Rapid hydrolysis → maleic acid formation Sealed bags for solid; N₂ blanket or desiccant-dried air for molten tanks; water ingress into molten tanks causes acid formation + violent boiling
Viscosity Solid (non-flowing) ~2–4 mPa·s (60–80°C) Molten MAH has very low viscosity - similar to water; easily pumped with standard centrifugal pumps; pipe sizes for low-viscosity hot liquid apply

⚖️ 4. Density & Viscosity

⚖️ Density Data
Solid density (20°C) 1.48 g/cm³
Liquid density (60°C) 1.314 g/cm³
Liquid density (80°C) 1.296 g/cm³
Liquid density (100°C) 1.278 g/cm³
Test method ASTM D1298 / pycnometer
1,000 kg solid → volume ~676 L (solid) → ~762 L (molten 60°C)
25 kg bag → volume solid ~16.9 L (compact solid)

Note the ~12.7% volume increase on melting. Heated storage tanks must be sized for the molten volume, not the bag volume.

💧 Viscosity of Molten MAH
Viscosity at 60°C ~3.5–4.0 mPa·s
Viscosity at 80°C ~2.5–3.0 mPa·s
Viscosity at 100°C ~1.8–2.2 mPa·s
Flow character Newtonian; water-like fluidity
Pump type Standard centrifugal; heat-traced lines
Pipe heat tracing Steam or electric; maintain ≥60°C throughout

Molten MAH is extremely low viscosity - take care at pipe joints; any leak will spread rapidly. All flanged connections in molten MAH systems must use chemical-resistant gaskets (PTFE).

📐 Specific Heat & Latent Heat
Specific heat (solid, 20°C) ~1.15 J/(g·K)
Specific heat (liquid, 70°C) ~1.50 J/(g·K)
Latent heat of fusion ~13.7 kJ/mol (140 J/g)
Heat of combustion ~1,390 kJ/mol
Heat of hydration (to maleic acid) ~59 kJ/mol (exothermic)

Hydration is moderately exothermic - water ingress into hot molten MAH generates heat + vapour; design heated tanks to prevent water contamination absolutely.

🌬️ 5. Vapour Pressure & Inhalation Risk

Temperature Vapour Pressure Phase Inhalation Risk Assessment
20 °C (ambient) < 0.01 mmHg Solid Negligible vapour; primary hazard is DUST from solid handling ✅ (if no dust generated)
55 °C (just above mp) ~0.05 mmHg Liquid (molten) Low vapour; OEL precautions begin; small heated melt pots should have local exhaust above 55°C
70 °C (typical melt temp) ~0.3 mmHg Liquid LEV (local exhaust ventilation) mandatory - theoretical air concentration at this VP can reach OEL rapidly in enclosed spaces ⚠️
100 °C ~2.5 mmHg Liquid Significant vapour generation; closed systems only; OV/P3 respirator if open work required; irritation immediate ⚠️
150 °C (synthesis) ~25 mmHg Liquid (in reactor) Closed reactor system only; condenser required to prevent MAH vapour loss and atmospheric contamination; reactor must be sealed

⚠️ MAH OEL (Occupational Exposure Limit): The ACGIH TLV-C (ceiling) for maleic anhydride is 0.1 ppm - a ceiling value that must never be exceeded. The EU IOELV (indicative OEL) is similarly very low. MAH is a respiratory sensitiser - repeated exposures at even sub-OEL concentrations can cause occupational asthma. Once sensitised, a worker may react to trace quantities that cause no symptoms in non-sensitised individuals. This is why MAH requires more rigorous inhalation control than most organic chemical intermediates, despite its relatively low volatility at ambient temperature.

💧 6. Solubility: Water Hydrolysis & Organic Solvents

⚠️ Water: Rapid Hydrolysis, NOT Simple Dissolution

When MAH contacts water, it does not simply dissolve - it immediately and irreversibly reacts to form maleic acid:

C₄H₂O₃ + H₂O → HOOC–CH=CH–COOH
(MAH + water → maleic acid; rapid; exothermic)

The resulting maleic acid solution is highly acidic (pH ~1.5 at 10% concentration). Key implications: (1) moisture in storage causes caking and quality loss; (2) MAH added to wet glassware or reactors generates acid immediately; (3) fire-fighting with water on large MAH fires creates maleic acid runoff - contain and neutralise with alkali; (4) for water treatment applications, MAH is first polymerised before contact with the process water.

✅ Organic Solvent Solubility
Solvent Solubility (approx.) Note
Acetone Very high (>500 g/L) Excellent solvent for MAH
Ethyl acetate High (~400 g/L) Good for analytical work
Chloroform High (~280 g/L) Research / analytical
Diethyl ether Moderate (~100 g/L) Recrystallisation solvent
Benzene / toluene Moderate (~80–120 g/L) SMA polymerisation solvent
Propylene glycol (PG) Reacts (ring-opening!) UPR synthesis basis
Mineral spirit / alkane Poor (<5 g/L, solid) Not suitable as carrier

⚡ 7. Chemical Reactivity Parameters

Reaction Type Reactant / Conditions Product Industrial Application
Hydration + H₂O; ambient temperature; fast Maleic acid (cis-diacid) Maleic acid production; poly-MAH synthesis intermediate; also an unwanted side reaction in storage
Esterification (ring-opening) + R–OH (glycol/alcohol); 60–100°C; fast ring opening → half-ester; then polycondensation at 160–220°C Half-ester → polyester (UPR) UPR synthesis - MAH's most important industrial reaction; rate much faster than phthalic anhydride esterification
Amidation + R–NH₂; ambient; very fast ring opening Maleamic acid half-amide MAH-g-polymer compatibiliser reactions with PA6/PA66; MAH-grafted PP reacts with nylon amine end groups in reactive extrusion
Imidisation + primary amine → maleamic acid → maleimide at >150°C N-substituted maleimide Bismaleimide (BMI) resins for aerospace composites; reactive diluents for high-temperature epoxy systems
Diels-Alder [4+2] + diene (cyclopentadiene, butadiene, terpenes); 0–80°C; no catalyst needed Bicyclic adduct (e.g., norbornene anhydride) Maleated rosin (tackifiers for hot-melt adhesives); specialty resin monomers; cyclopentadiene/MAH adduct used as MAH storage form
Free-radical copolymerisation + styrene or vinyl ether; peroxide initiator; 60–120°C SMA, PVME-MAH, PIB-MAH copolymers SMA engineering plastics; scale inhibitors; dispersion agents; MAH is an excellent radical acceptor due to electron-poor C=C
Grafting (radical) + PP/PE + peroxide; reactive extrusion 180–220°C; 0.5–2% MAH loading MAH-g-PP; MAH-g-PE Compatibilisers for glass-filled PP composites; PA6/PP alloys; adhesive tie-layers in multilayer films
Isomerisation Maleic acid + heat (>150°C) or acid catalyst Fumaric acid (trans isomer) Fumaric acid production; occurs partially during high-temperature UPR synthesis (converts some maleate to fumarate units, which actually improves UPR properties)

⚠️ Incompatible Materials - Do Not Mix With MAH

Water / moisture
Rapid hydrolysis to maleic acid; exothermic; causes violent boiling if water enters hot molten MAH
Strong bases (NaOH, KOH)
Rapid ring-opening neutralisation; exothermic; generates sodium/potassium maleate
Strong oxidisers
H₂O₂, KMnO₄ - exothermic reactions; risk of fire or explosion with molten MAH
Primary amines
Rapid ring-opening to maleamic acids; normally intentional (grafting applications) but exothermic - control temperature
Glycols / polyols
Reactive (intended for UPR synthesis) - do not mix in uncontrolled environment; ring-opening is exothermic and fast
Aluminium, copper alloys
Maleic acid (from MAH hydrolysis) corrodes these metals - use stainless steel 316L or glass-lined equipment ✅

🔬 8. Spectroscopic & Optical Properties

📡 FTIR Key Absorptions
Anhydride C=O asymm. stretch 1,850 cm⁻¹ (strong)
Anhydride C=O symm. stretch 1,780 cm⁻¹ (strong)
C=C stretch (ring) 1,630–1,650 cm⁻¹
C–O–C anhydride stretch 1,000–1,100 cm⁻¹
=C–H stretch 3,100–3,150 cm⁻¹
Diagnostic feature Twin C=O bands at 1,780 + 1,850 confirm cyclic anhydride

The twin carbonyl bands (doublet at ~1,780 and ~1,850 cm⁻¹) are the definitive FTIR signature of a cyclic anhydride; if one band is absent or shifted, the ring may be opened (maleic acid contamination).

🧲 ¹H NMR (CDCl₃)
Vinyl protons (H–C=C–H) δ 7.52 ppm (singlet, 2H)
No other protons Minimal spectrum - only vinyl H present
¹³C NMR δ 163 ppm (C=O); δ 135 ppm (C=C)

The ¹H NMR of MAH is exceptionally simple - a single singlet at δ 7.52 ppm for the two equivalent vinyl protons. Any additional peaks indicate impurities (maleic acid at ~6.3 ppm, fumaric acid at ~6.7 ppm).

🔭 Other Physical Constants
Refractive index (liquid, 70°C) nD⁷⁰ ~1.4440
Colour (APHA, molten) ≤30 (standard); ≤10 (premium)
UV absorption (max) ~215 nm (strong); ~290 nm (weak)
pKa (maleic acid, 1st) 1.94 (strong acid)
pKa (maleic acid, 2nd) 6.22
Dipole moment ~3.95 D (in benzene)

Maleic acid (formed by MAH hydrolysis) is a strong acid (pKa₁ 1.94) - solutions are highly acidic; standard acid-resistant materials of construction required.

🧪 9. Incoming QC Testing Methods & Acceptance Criteria

Test Method Standard Grade Premium Grade Time Notes
Crystallisation point ⭐ ASTM E794; melt and slowly cool ≥ 52.5 °C ≥ 52.6 °C 20 min Primary purity indicator - mandatory every batch; fail = reject
Purity (MAH%) ⭐ GC-FID or titrimetric (acid-base) ≥ 99.0% ≥ 99.5% 30–45 min Titrimetric method: dissolve in water, titrate with NaOH to two endpoints; GC confirms identity of impurities
Colour (APHA) ASTM D1209; measure molten sample at 70°C ≤ 30 ≤ 10 15 min Must be measured molten - solid colour is not representative. Coloured MAH causes yellow UPR and may indicate iron contamination
Maleic acid content GC-FID; dissolve in acetone; compare peak areas ≤ 0.3% ≤ 0.1% 30 min High maleic acid = moisture damage in transit; also correlates with suppressed crystallisation point; causes cloudy UPR
Iron (Fe) ICP-OES; acid digest sample ≤ 5 ppm ≤ 1 ppm 1–2 days Fe causes colour development in UPR; catalyses premature polymerisation of inhibitor; critical for gel-coat grade; outsource to accredited lab quarterly
Ash ASTM D482; ignite at 800°C ≤ 0.005% ≤ 0.003% 2–3 h Trace metals summary test; if ash is above spec, run ICP-OES to identify specific metals (Fe, V, Mo from catalyst residues)
Appearance Visual inspection White solid, free-flowing flakes; no lumps, no discolouration White, uniform flakes 2 min Yellow or grey discolouration → iron contamination or moisture damage; hard lumps → caking from moisture; reject and investigate

💡 Rapid 30-minute incoming QC protocol for MAH: (1) Visual check (2 min): white free-flowing flakes, no discolouration, no caking - if yellow or grey, run Fe ICP before releasing; (2) Crystallisation point (20 min): melt ~5g sample, slowly cool while recording temperature - must crystallise at ≥52.5°C; if below 52°C, reject (moisture damage); (3) APHA colour (10 min): inspect molten sample against standard - must be ≤30 APHA for standard grade. These three tests together take under 35 minutes and catch the most common MAH quality failures: moisture damage, iron contamination, and blending/substitution.

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❓ 10. Frequently Asked Questions

Q1: What is the melting point of maleic anhydride?

The melting point of maleic anhydride is 52.8 °C (127 °F). This is commercially the most important physical property of MAH because it determines whether the material is handled as a solid or as a liquid in any given environment. At typical ambient temperatures of 20–25 °C, MAH is a solid white crystalline material. In summer warehouses, containers, or heated transport vehicles that reach temperatures above 52.8 °C, MAH can partially or fully melt - causing bag deformation, leakage from damaged bags, and potential caking on re-solidification. For industrial processing (UPR synthesis, esterification, SMA polymerisation), MAH must be melted in heated vessels at 60–80 °C before addition to the reactor. The crystallisation point (≥52.5 °C for standard commercial grade; ≥52.6 °C for premium grade) is the key QC specification for purity: a suppressed crystallisation point below 52 °C indicates contamination with maleic acid (formed by hydrolysis from moisture exposure) or fumaric acid, both of which act as freezing-point depressants and are reject criteria.

Q2: What is the boiling point of maleic anhydride?

The boiling point of maleic anhydride at atmospheric pressure (760 mmHg) is 202 °C. This is considerably higher than the typical processing temperatures used in most MAH applications (60–180 °C for UPR synthesis, 60–120 °C for SMA polymerisation), which means that MAH does not boil off or evaporate significantly during normal industrial use. The high boiling point also means that product loss by evaporation from synthesis reactors is minimal at process temperatures, and that MAH can be used as a component in high-temperature bake-cure systems without loss. For distillation or purification purposes - used to upgrade off-spec or recovered MAH - vacuum distillation is employed, reducing the effective boiling point to approximately 80–100 °C at 1–5 mmHg operating pressure, making the purification energy-efficient and avoiding thermal decomposition above 280 °C. The combination of melting point (52.8 °C) and boiling point (202 °C) defines MAH's processing window: it is a low-melting solid that can be easily liquefied and processed as a mobile liquid over a very wide temperature range (53–200 °C) without significant vapour loss.

Q3: What happens when maleic anhydride contacts water?

When maleic anhydride contacts water, it does not simply dissolve - it reacts rapidly and irreversibly to form maleic acid: C₄H₂O₃ + H₂O → HOOC–CH=CH–COOH (maleic acid). This hydrolysis reaction is exothermic (~59 kJ/mol), fast at ambient temperature, and nearly instantaneous with warm water. The resulting maleic acid solution is strongly acidic (pH ~1.5 at 10% concentration, due to maleic acid's first pKa of 1.94). Practical implications of this behaviour: (1) Storage: MAH bags must be kept sealed and dry; even moderate humidity causes surface hydrolysis, caking, and quality loss; bag leaks in rain or high-humidity environments cause significant maleic acid contamination; (2) Process design: water must be completely excluded from heated MAH tanks; if water enters a hot molten MAH tank, violent exothermic hydrolysis + steam generation can cause a boil-over; (3) Fire response: using water on MAH fires generates acidic maleic acid runoff that must be contained and neutralised; CO₂ or dry powder extinguishers are preferred; (4) Quality control: a suppressed crystallisation point (below 52°C) indicates moisture damage has occurred during storage or transport.

Q4: How do I identify maleic anhydride from maleic acid by FTIR?

Maleic anhydride and maleic acid have distinctly different and definitive FTIR spectra. Maleic anhydride: The diagnostic feature is the cyclic anhydride doublet - two strong C=O stretching bands at approximately 1,850 cm⁻¹ (asymmetric) and 1,780 cm⁻¹ (symmetric). These twin carbonyl bands are the hallmark of any cyclic anhydride; both bands must be present to confirm the anhydride ring is intact. Additionally: C=C stretch at 1,630–1,650 cm⁻¹; C–O–C anhydride stretch at 1,000–1,100 cm⁻¹; vinyl =C–H stretch at 3,100–3,150 cm⁻¹. Maleic acid (hydrolysis product): The twin anhydride bands at 1,780 and 1,850 cm⁻¹ are absent; instead, a broad carboxylic acid O–H stretch appears at 2,500–3,300 cm⁻¹ and a single C=O stretch of the diacid appears at ~1,710 cm⁻¹. If your MAH sample shows a shoulder or peak at 1,710 cm⁻¹ alongside the 1,780/1,850 bands, it indicates partial hydrolysis to maleic acid has occurred. For quantification of maleic acid content in MAH, GC-FID analysis of an acetone solution is more precise than FTIR.

Q5: What is the density of maleic anhydride and how do I calculate tank volumes?

Maleic anhydride has two relevant density values: solid density 1.48 g/cm³ at 20 °C, and molten liquid density 1.31 g/cm³ at 60 °C. For volume calculations: 1 metric tonne (1,000 kg) of solid MAH occupies approximately 676 litres (as compact solid). When melted at 60 °C, the same 1,000 kg occupies approximately 763 litres - an 11–13% volume increase on melting. This means heated storage tanks must be sized for the molten density, not the solid density. Example: a heated MAH storage tank designed for 5 MT holding capacity must accommodate at least 3,815 litres (5,000 kg ÷ 1.31 g/cm³ × 1,000 mL/L). Add a 10–15% safety headspace for thermal expansion during temperature variations, bringing the practical tank volume to ~4,200 litres for a 5 MT MAH storage tank. For volumetric metering of molten MAH into reactors, use the temperature-corrected density (1.31 at 60°C, 1.30 at 70°C, 1.28 at 80°C) for accurate mass conversion.

Q6: What QC tests should I run on received maleic anhydride before using it in UPR synthesis?

For UPR synthesis, a minimum three-test incoming QC protocol is recommended and can be completed in under 35 minutes: (1) Visual inspection: confirm white, free-flowing flakes with no yellow/grey discolouration (yellow = iron contamination; grey = catalyst residue) and no large lumps (lumps indicate moisture damage and caking); (2) Crystallisation point (most important test, 20 minutes): melt approximately 5 g of sample in a glass test tube at 65°C; insert a calibrated thermometer; allow to cool slowly while gently stirring; record the temperature at which the first crystals appear - must be ≥52.5°C for standard grade; a crystallisation point of 52.0°C or below indicates maleic acid contamination from moisture exposure and the batch should be rejected or segregated; (3) APHA colour of melt (10 minutes): keep the sample molten at 70°C and compare against APHA platinum-cobalt colour standards - must be ≤30 APHA for standard grade; ≤10 for premium/gel-coat grade. If visual inspection reveals discolouration, additionally run iron by ICP-OES before releasing. These three tests catch the three most common MAH quality failures: moisture damage (crystallisation point), iron contamination (colour + visual), and substitution with lower-grade material (both tests combined). Provide the batch COA to your synthesis team for the exact purity value used in stoichiometric calculations.

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Crystallisation point ≥52.5°C · Fe ≤5 ppm · 25 kg bags & big bags · REACH OR · Class 4.1 DG docs

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